2006
DOI: 10.1002/ceat.200600109
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Heterogeneously Catalyzed Esterification of FFAs in Vegetable Oils

Abstract: The production of methyl esters (biodiesel) from free fatty acids (FFAs) contained in vegetable oils was studied using a heterogeneous acid catalyst. The feedstock was a by-product of a vegetable oil refinery. The experiments were performed in a batch reactor, in a temperature range of 363.15-393.15 K, with an initial molar ratio of methanol to FFAs of 6.6/1, while the catalyst mass was fixed at 2 wt % of the total vegetable oil mass. A technical kinetic model has been developed which accounts for the reversib… Show more

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Cited by 65 publications
(36 citation statements)
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“…Hence, the assumption of absence of external and internal mass-transfer resistances in model development is confirmed because this reaction is established as kinetically controlled. [26][27][28] Pasias et al 17 used the same reaction model for the esterification of FFAs in vegetable oil with methanol using cationexchange resin as catalyst. They reported activation energies of forward and backward reactions of 70.34 and 37.93 kJ mol 21 , respectively.…”
Section: Kinetic Parameters Estimationmentioning
confidence: 99%
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“…Hence, the assumption of absence of external and internal mass-transfer resistances in model development is confirmed because this reaction is established as kinetically controlled. [26][27][28] Pasias et al 17 used the same reaction model for the esterification of FFAs in vegetable oil with methanol using cationexchange resin as catalyst. They reported activation energies of forward and backward reactions of 70.34 and 37.93 kJ mol 21 , respectively.…”
Section: Kinetic Parameters Estimationmentioning
confidence: 99%
“…15 This result is consistent with the literature reported. 15,17,24,25 Activation Energy. As aforementioned, the forward reaction rate and equilibrium constants depending on temperature are represented by the Arrhenius model (Eqs.…”
Section: Kinetic Parameters Estimationmentioning
confidence: 99%
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“…Üblicherweise werden natürliche Fette und Öle mit Methanol und alkalischen homogenen Katalysatoren umgesetzt, um Fettsäureme-thylester (FAME) mit der entsprechenden Spezifikation zu erzeugen. Heute werden bevorzugt raffiniertes Sojabohnen-, Raps-, Sonnenblumen-und Palmöl für Biodiesel eingesetzt [1]. Von Nachteil sind dabei die hohen Kosten des Einsatzöls.…”
Section: Problemstellungunclassified